中空纤维Silicalite-1分子筛膜用于轻石脑油中烷烃的分离 |
作者:孙耀璋1, 吕舒远1, 张春1, 李金芝2, 胡锐1, 于中伟2, 顾学红1 |
单位: 1. 南京工业大学 化工学院 材料化学工程国家重点实验室,南京 211800; 2. 中石化石油化工科学研究院有限公司,北京 100083 |
关键词: 中空纤维; Silicalite-1分子筛膜; 轻石脑油; 蒸汽渗透; 烷烃分离 |
DOI号: 10.16159/j.cnki.issn1007-8924.2025.02.013 |
分类号: TQ028.1 |
出版年,卷(期):页码: 2025,45(2):109-116 |
摘要: |
轻石脑油中富含C5、C6烷烃,开发高效节能的分离技术将正、异构体分开,实现工业产品的物尽其用是人们关注的焦点。本文在四通道中空纤维载体上制备了Silicalite-1(全硅型MFI)分子筛膜,并将其用于C5、C6烷烃正异构体的分离,考察了温度、压力等操作条件对所制备分子筛膜性能的影响。结果表明,对于正戊烷/异戊烷(n-/i-C5)二元体系的分离,在80 ℃,原料分压为5 kPa时,n-C5渗透性为1.12×10-7 mol/(m2·s·Pa),n-/i-C5分离因子可达109;对于正己烷/三甲基戊烷/二甲基戊烷(n-C6/3MP/2MP)三元体系的分离,在80 ℃,原料分压为5 kPa时,n-C6的渗透性为1.83×10-7 mol/(m2·s·Pa),n-/i-C6分离因子高达132。同时,评价了较高进料分压下所制备膜材料在分离体系中的运行稳定性,均可稳定操作60 h以上。该研究结果将为石化行业的技术革新升级奠定基础。 |
Light naphtha is rich in C5 and C6 alkanes, so it is focused to develop the efficient and energy-saving technologies of separating n-alkane and i-alkanes. It will be helpful to realize the best use of industrial product. In this paper, Silicalite-1 (all-silica MFI) zeolite membranes were prepared on four-channel hollow fiber substrates and used for the separation of C5 or C6 alkane mixtures. Besides, the effects of operating conditions such as temperature and pressure on the performance of the prepared zeolite membranes were investigated. For the separation of n-pentane/isopentane (n-/i-C5) binary mixture, a n-C5 permeance of 1.12×10-7 mol/(m2·s·Pa) and the n-/i-C5 separation factor of 109 were achieved at 80 ℃ and the feed partial pressure of 5 kPa. For the separation of n-hexane/trimethylpentane/dimethylpentane (n-C6/3MP/2MP) ternary mixture at 80 ℃ and the 5 kPa feed partial pressure, the membrane showed a n-C6 permeance of 1.83×10-7 mol/(m2·s·Pa) and a n-/i-C6 separation factor of 132. At the same time, the operation stability under high feed partial pressure was evaluated. And the long-term stable operation can last more than 60 h. The results of this study will lay a foundation for technological innovation and upgrading in the petrochemical industry. |
基金项目: |
中国石油化工股份有限公司委托项目(124056) |
作者简介: |
孙耀璋(2001-),男,甘肃陇西人,硕士研究生,主要研究方向为分子筛膜的制备及应用 |
参考文献: |
[1]邢卫红, 顾学红. 高性能膜材料与膜技术[M]//北京: 化学工业出版社, 2017. [2]Li Y C, Zhu G F, Wang Y, et al. Preparation, mechanism and applications of oriented MFI zeolite membranes: a review[J]. Micropor Mesopor Mater, 2021, 312: 110790. [3]Wu Z Q, Zhang C, Peng L, et al. Enhanced stability of MFI zeolite membranes for separation of ethanol/water by eliminating surface Si-OH groups[J]. ACS Appl Mater Interfaces, 2018, 10 (4): 3175-3180. [4]Zhang H X, Oh Y J, Tikue E T, et al. Enrichment of spent SF6 gas by zeolite membranes for direct reuse in gas-insulated switchgear units[J]. Sep Purif Technol, 2022, 303: 122223. [5]韩奎奎, 谭湘龙, 李金芝, 等.四通道中空纤维MFI分子筛膜用于二甲苯异构体分离[J]. 化工学报, 2023, 74(6): 2468-2476. [6]Hong Z, Zhang C, Gu X H, et al. A simple method for healing nonzeolitic pores of MFI membranes by hydrolysis of silanes[J]. J Membr Sci, 2011, 366(1/2): 427-435. [7]Jareman F, Hedlund J, Sterte J. Effects of aluminum content on the separation properties of MFI membranes[J]. Sep Purif Technol, 2003, 32(1): 159-163. [8]Mori N, Tomita T. Separation of n-butane/iso-butane by self-supporting MFI membranes with various SiO2/Al2O3[J]. Micropor Mesopor Mater, 2008,112(1/2/3): 88-96. [9]Bowen T C, Kalipcilar H, Falconer J L, et al. Separation of C4 and C6 isomer mixtures and alcohol-water solutions by monolith supported B-ZSM-5 membranes[J]. Desalination, 2002, 147(1/2/3): 331-332. [10]Sommer S, Melin T, Falconer J L, et al. Transport of C6 isomers through ZSM-5 zeolite membranes[J]. J Membr Sci, 2003, 224(1/2): 51-67. [11]Noack M, Klsch P, Seefeld V, et al. Influence of the Si/Al-ratio on the permeation properties of MFI-membranes[J]. Micropor Mesopor Mater, 2005, 79(1/2/3): 329-337. [12]Arruebo M, Falconer J L, Noble R D. Separation of binary C5 and C6 hydrocarbon mixtures through MFI zeolite membranes[J]. J Membr Sci, 2006,219(1/2): 171-176. [13]Bayati B, Belbasi Z, Ejtemaei M, et al. Separation of pentane isomers using MFI zeolite membrane[J]. Sep Purif Technol, 2013, 106: 56-62. [14]Coronas J, Noble R D, Falconer J L. Separations of C4 and C6 isomers in ZSM-5 tubular membranes[J]. Ind Eng Chem Res, 1998, 37:166-176. [15]Rong H, Wang G, Yan J, et al. Surface-gel-conversion synthesis of submicron-thick MFI zeolite membranes to expedite shape-selective separation of hexane isomers[J]. Sci China Mater, 2021, 64(2): 374-382. [16]Shi Z Z, Zhang Y T, Cai C, et al. Preparation and characterization of α-Al2O3 hollow fiber membranes with four-channel configuration[J]. Ceram Int, 2015, 41(1): 1333-1339. [17]Cai C, Zhang Y T, Zhang C, et al. Microstructure modulation of α-Al2O3 hollow fiber membranes with four-channel geometric configuration[J]. Asia-Pac J Chem Eng, 2016, 11(6): 949-957. [18]陈园园, 时振洲, 张春, 等. 相转化凝固浴对Al2O3中空纤维多孔载体微观结构的影响[J]. 无机材料学报, 2014, 29(2): 143-148. [19]Liu D Z, Zhang Y T, Jiang J, et al. High-performance NaA zeolite membranes supported on four-channel ceramic hollow fibers for ethanol dehydration[J]. RSC Adv, 2015, 5: 95866-95871. [20]Liu H, Gao X C, Wang S X, et al. SSZ-13 zeolite membranes on four-channel α-Al2O3 hollow fibers for CO2 separation[J]. Sep Purif Technol, 2021, 267: 118611. [21]Cavalcante C L J, Ruthven D M. Adsorption of branched and cyclic paraffins in Silicalite-1 equilibrium[J]. Ind Eng Chem Res, 1995, 34:177-184. [22]Mabande G T P, Noack M, Avhale A, et al. Permeation properties of bi-layered Al-ZSM-5/Silicalite-1 membranes[J]. Micropor Mesopor Mater, 2007, 98(1): 55-61. [23]Yu K, Xiao H, Ding J, et al. Efficient separation of linear and mono-branched hexane isomers using large-area silicalite-1 membranes[J]. Sep Purif Technol, 2025, 354(5): 129115. |
服务与反馈: |
【文章下载】【加入收藏】 |
《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com
京公网安备11011302000819号